Method for separating estrogen from placenta

ABSTRACT

The present invention provides a method of separating estrogen from placenta, which uses supercritical fluid technique to load the placenta powder of human body or sheep, pig, deer and other animals into an extraction tank. Under the operating conditions of preset pressure and temperature, supercritical solvent is added into the extraction tank to extract estrogen from placenta, so as to acquire de-estrogen placenta powder and placenta extract liquor. Under the same condition, the de-estrogen placenta extract liquor and supercritical solvent are added by a preset volume flow ratio into an adsorption tank. The estrogen in the placenta extract liquor is adsorbed by the adsorption tank to obtain de-estrogen placenta extract. It is then eluted with ethanol solution by gradient proportion to obtain purified natural estrogen.

The current application claims a foreign priority to the patent application of Taiwan No. 103112021 filed on Mar. 31, 2014.

BACKGROUND OF INVENTION

1. Field of the Invention

The present invention relates generally to a technology of separating estrogen from placenta, and more particularly to a method which can not only reduce or remove estrogen from placenta, but also deodorize, remove bitterness, enhance the taste, and ensure food safety.

2. Description of Related Art

Placenta contains a wide range of bioactive ingredients, and may produce almost all substances that can be found in any human organ to support the growth and development of the fetus in the mother's womb. This biochemical treasure supplies substances to the growing fetus that cannot be generated by itself. Placenta also contains a variety of enzymes that support the metabolism of steroid hormones, such as estrogen and progesterone. Placenta can also adjust the body's functional state, enhance body immunity, and resist allergy. Scientific studies showed that extracts obtained from the placenta can be widely used in biomedical/medical areas such as for whitening, moisturizing and accelerating cell healing and regeneration, regulating the female endocrine, fully and effectively improving the human skin-aging, promoting skin whitening, increasing skin elasticity, preventing wrinkles and enhancing cell activities, resisting allergies and tumors, and improving memory.

Moreover, the ingredient of estrogen is Estrogens. In recent years, women realize that they must supplement additional hormone to replenish the decreasing estrogen after menopause. However, the hormone replacement therapy has been stopped recently in the U.S. because research shows that long-term hormone supplementation may cause cancer. According to American FDA's requirement, Estrogens content in cosmetic products should be less than 10,000 IU/ounce.

For the conventional technologies of separating and removing estrogen from placenta as shown in U.S. Pat. No. 4,784,960, U.S. Pat. No. 4,423,151, U.S. Pat. No. 5,565,199 and No. 20070087001, No. 20040132086, most methods separate estrogen from placenta with strong acid, strong base, and enzyme or by heating and adding organic solvent. Estrogen ingredients may be decomposed when treated with acid, alkali and enzyme, and then separated with organic solvent requiring 100-1000 times of aqueous solution or solvent for de-estrogen. Following de-estrogen, subsequent complicated concentration, separation and purification procedures are required. The damage of acid and alkali on effective functional ingredients and enzyme activity should be taken into consideration, thus, mass production is infeasible.

SUMMARY OF THE INVENTION

The primary objective of the present invention is to provide a method of separating estrogen from placenta, which adopts safe and nontoxic supercritical solvent with physical extraction at high pressure/low temperature and separation at low pressure/low temperature without the need of complicated solvent removal, concentration, and separation procedures. Moreover, there is no concern about the residual solvent. The supercritical solvent is recyclable; thus, said method is environmentally-friendly, safe, and practical.

The present invention provides a method of separating estrogen from placenta, which comprising: Estrogen extraction: under the operating conditions of preset temperature and pressure, load placenta powder in an extraction tank, and add supercritical solvent to extract estrogen from placenta powder, and produce placenta extract liquor; adsorption: under the same operating condition, add the extract liquor of de-estrogen placenta and supercritical solvent into an adsorption tank, allow the estrogen in the placenta extract liquor to be adsorbed by the adsorption tank, so as to remove de-estrogen placenta extract; gradient elution: elute the estrogen in the adsorption tank with gradient proportion ethanol solution for desorption of the estrogen, so as to obtain purified natural estrogen.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a flow chart of a preferred embodiment of the present invention.

FIG. 2 is a diagram, showing the estrogen rejection data.

FIG. 3 is a diagram, showing the analysis of de-fishy aroma, color and bitterness and the other data.

DETAILED DESCRIPTION OF THE INVENTION

The following is the detailed description of a preferred embodiment of the present invention with reference to the accompanying drawings:

FIG. 1 shows a preferred embodiment of the method for separating estrogen from placenta 100, whereby estrogen can be removed from placenta to acquire de-estrogen placenta powder, placenta extract and purified estrogen.

Step 1 extraction 110: under the operating pressure of 20-30 MPa (e.g., 20, 22, 24, 26, 28, 30 MPa) and at the temperature of 40° C., load 1 Kg placenta powder into an extraction tank and add supercritical solvent into the extraction tank by a volume flow ratio of 10-20:1, so as to extract estrogen from placenta powder and produce placenta extract liquor after 2-3 h reaction time. The placenta powder may be dry placenta powder of human body or sheep, pig, deer or other animals. The supercritical solvent is a supercritical carbon dioxide (SC-CO₂)/ethanol solvent. The extraction tank is a stainless steel tank of ID 60 mm, OD 130 mm and height 130 mm filled with stainless steel monomer pieces.

Step 2 adsorption 120: under the same operating condition (pressure 20-30 MPa and temperature 40° C.), add the de-estrogen placenta extract liquor and supercritical solvent into an adsorption tank by a volume flow ratio of 10-20:1, allow the estrogen in the placenta extract liquor to be adsorbed by the adsorption tank to acquire de-estrogen placenta extract. The adsorption tank is a stainless steel tank of ID 36 mm, OD 48 mm and height 597 mm filled with silica gel, sephadex or resin and other adsorbents that can adsorb estrogen.

Step 3 gradient elution 130: after the estrogen is adsorbed in the adsorption tank, elute 50% ethanol solution to 80% ethanol solution by gradient proportion to acquire purified natural estrogen.

The following is an implementation of said method under different operating conditions (changing the pressure and volume flow ratio of supercritical solvent). The residual extracting and extracted examples are quantitatively analyzed for their estrogen concentration and color change. The estrogen concentration is quantified by ELISA on progesterone and estriol. The color is measured with Japan-made Denshoku Σ90 colorimeter, indicated by Hunter L, a, b value. The color L value closer to 100 indicates a higher sample transparency. Sensory evaluations for acceptance including odor (fishy aroma), bitterness, color and overall are rated. The rating is from 0 to 10, where 10 is the most acceptable, and 0 is the most unacceptable. The highest rejection of estrogen (%), deodorization, bitterness removal, and overall acceptance are selected to evaluate the optimal reaction condition:

FIG. 2 depicts the estrogen rejection data. When the pressure is 24-26 MPa and temperature is 40° C., and the volume flow ratio of supercritical solvent is 15:1, which is the optimal operating condition, the rejection rate may reach 90%. This is mainly because the supercritical solvent under high pressure exerts high solubility and mass transportation rate, and under low temperature has low viscosity and high density of supercritical fluid, which may increase the reactant contract opportunity to accelerate the removal of estrogen from placenta powder. Therefore, the supercritical solvent under high pressure and low temperature may resolve the shortcomings when using larger number of organic solvent in hydrolyzing estrogen with acid, alkali and enzyme.

In addition, the color change data of placenta before and after extraction measured with a colorimeter are shown in Table 1. The de-estrogen sample color L value is 62.4, which is higher than placenta powder color L value of 39.2 before processing. This suggests that the de-estrogen sample presents higher transparency. According to Table 1, the de-estrogen sample in present invention has deodorization, bitterness removal, high color and overall acceptance.

TABLE 1 Analytical Items Placenta Powder SC-CO2/EtOH Color L 39.2 62.4 a 17.2 14.6 b 44.7 44.2 Acceptance evaluation Odor 1.5 8.4 Color 6.8 8.2 Bitterness 1.7 7.4 Overall 3.7 8.1

As shown in FIG. 3, the de-estrogen sample and extract prepare in the present invention has bright appearance, deodorized taste without bitterness, de-estrogen and good acceptance, unlike the placenta powder with odor and bitter taste, and estrogen ingredient.

The method of the present invention for separating estrogen from placenta uses safe and nontoxic supercritical solvent. Physical extraction, adsorption and gradient elution are used to prepare de-estrogen placenta and its extract under supercritical CO₂, which exerts the properties of high solubility, low viscosity and high mass transportation efficiency and no safety concern of residual solvent. The environmentally friendly and safe supercritical solvent can be recycled. Compared with the conventional method of using acid, alkali and enzyme for decomposition, and using organic solvent for separation, which may lead to safety concern of residual solvent, the present invention is an improved method and has practical value. 

1. A method of separating estrogen from placenta using a supercritical fluid, comprising the following steps: extraction: under the operating conditions of preset temperature and pressure, load placenta powder in an extraction tank, add supercritical solvent to extract estrogen from placenta powder, and produce placenta extract liquor, wherein said placenta powder is a dry placenta powder of human body or sheep, pig, deer or other animals, and wherein said supercritical solvent is supercritical carbon dioxide/ethanol, and in the extraction step, it is required to load 1 Kg placenta powder in an extraction tank under the operating condition of 20-30 MPa and 40° C., add supercritical solvent into an adsorption tank by a volume flow ratio of 10˜20:1, extract estrogen after for 2-3 h reaction time; adsorption: under the same operating condition, add the extract liquor of de-estrogen placenta and supercritical solvent into an adsorption tank, allow the estrogen in the placenta extract liquor to be adsorbed by the adsorption tank, obtain the de-estrogen placenta extract, wherein said adsorbent may be silica gel, sephadex or resin and other adsorbent that can adsorb estrogen; and gradient elution: elute the estrogen in the adsorption tank with gradient proportion ethanol solution for desorption of the estrogen, obtain purified natural estrogen, wherein said ethanol solution is eluted by gradient proportion from 50% to 80%.
 2. (canceled)
 3. (canceled)
 4. The method defined in claim 3, wherein, in the extraction step, the optimal operating condition is: pressure of 24˜26 MPa, temperature of 40° C., and the volume flow ratio of supercritical solvent of 15:1, the rejection can reach 90%
 5. The method defined in claim 3, wherein said extraction tank is a stainless steel tank with an internal diameter of 60 mm, external diameter of 130 mm and height of 130 mm, filled with stainless steel monomer pieces.
 6. The method defined in claim 4, wherein said extraction tank is a stainless steel tank with an internal diameter of 60 mm, external diameter of 130 mm and height of 130 mm, filled with stainless steel monomer pieces.
 7. The method defined in claim 1, wherein, in the adsorption step, said adsorption tank is a stainless steel tank with an internal diameter of 36 mm, external diameter of 48 mm and height of 597 mm, filled with adsorbent that can adsorb estrogen.
 8. (canceled)
 9. (canceled)
 10. (canceled) 